WO2022186971A1 - Système de régulation de débit de fluide comprenant un ensemble collecteur - Google Patents

Système de régulation de débit de fluide comprenant un ensemble collecteur Download PDF

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Publication number
WO2022186971A1
WO2022186971A1 PCT/US2022/016286 US2022016286W WO2022186971A1 WO 2022186971 A1 WO2022186971 A1 WO 2022186971A1 US 2022016286 W US2022016286 W US 2022016286W WO 2022186971 A1 WO2022186971 A1 WO 2022186971A1
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WO
WIPO (PCT)
Prior art keywords
outlet
port
vacuum
fluidly coupled
controlling flow
Prior art date
Application number
PCT/US2022/016286
Other languages
English (en)
Inventor
Philip Ryan BARROS
Greg Patrick MULLIGAN
Original Assignee
Ichor Systems, Inc.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Ichor Systems, Inc. filed Critical Ichor Systems, Inc.
Priority to KR1020237031210A priority Critical patent/KR20230150309A/ko
Priority to JP2023553151A priority patent/JP2024512898A/ja
Publication of WO2022186971A1 publication Critical patent/WO2022186971A1/fr

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Classifications

    • GPHYSICS
    • G05CONTROLLING; REGULATING
    • G05DSYSTEMS FOR CONTROLLING OR REGULATING NON-ELECTRIC VARIABLES
    • G05D7/00Control of flow
    • G05D7/06Control of flow characterised by the use of electric means
    • G05D7/0617Control of flow characterised by the use of electric means specially adapted for fluid materials
    • G05D7/0629Control of flow characterised by the use of electric means specially adapted for fluid materials characterised by the type of regulator means
    • G05D7/0635Control of flow characterised by the use of electric means specially adapted for fluid materials characterised by the type of regulator means by action on throttling means
    • G05D7/0641Control of flow characterised by the use of electric means specially adapted for fluid materials characterised by the type of regulator means by action on throttling means using a plurality of throttling means
    • G05D7/0652Control of flow characterised by the use of electric means specially adapted for fluid materials characterised by the type of regulator means by action on throttling means using a plurality of throttling means the plurality of throttling means being arranged in parallel
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F16ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
    • F16KVALVES; TAPS; COCKS; ACTUATING-FLOATS; DEVICES FOR VENTING OR AERATING
    • F16K27/00Construction of housing; Use of materials therefor
    • F16K27/003Housing formed from a plurality of the same valve elements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F16ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
    • F16KVALVES; TAPS; COCKS; ACTUATING-FLOATS; DEVICES FOR VENTING OR AERATING
    • F16K37/00Special means in or on valves or other cut-off apparatus for indicating or recording operation thereof, or for enabling an alarm to be given
    • F16K37/0025Electrical or magnetic means
    • F16K37/005Electrical or magnetic means for measuring fluid parameters
    • GPHYSICS
    • G05CONTROLLING; REGULATING
    • G05DSYSTEMS FOR CONTROLLING OR REGULATING NON-ELECTRIC VARIABLES
    • G05D7/00Control of flow
    • G05D7/06Control of flow characterised by the use of electric means
    • G05D7/0617Control of flow characterised by the use of electric means specially adapted for fluid materials
    • G05D7/0629Control of flow characterised by the use of electric means specially adapted for fluid materials characterised by the type of regulator means
    • G05D7/0635Control of flow characterised by the use of electric means specially adapted for fluid materials characterised by the type of regulator means by action on throttling means
    • G05D7/0641Control of flow characterised by the use of electric means specially adapted for fluid materials characterised by the type of regulator means by action on throttling means using a plurality of throttling means
    • G05D7/0658Control of flow characterised by the use of electric means specially adapted for fluid materials characterised by the type of regulator means by action on throttling means using a plurality of throttling means the plurality of throttling means being arranged for the control of a single flow from a plurality of converging flows
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01LSEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
    • H01L21/00Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
    • H01L21/67Apparatus specially adapted for handling semiconductor or electric solid state devices during manufacture or treatment thereof; Apparatus specially adapted for handling wafers during manufacture or treatment of semiconductor or electric solid state devices or components ; Apparatus not specifically provided for elsewhere
    • H01L21/67005Apparatus not specifically provided for elsewhere
    • H01L21/67011Apparatus for manufacture or treatment
    • H01L21/67017Apparatus for fluid treatment

Definitions

  • Mass flow control has been one of the key technologies used in semiconductor chip fabrication. Apparatuses for controlling mass flow are important for delivering known flow rates of process gases and liquids for semiconductor fabrication and other industrial processes. Such devices are used to measure and accurately control the flow of fluids for a variety of applications. In a given fabrication tool, a variety of liquids and gases might be required. As a result, efficient gas and liquid handling is essential to modern semiconductor fabrication equipment.
  • the present technology is directed to systems for processing articles such as semiconductors. In other embodiments, the present technology is directed to systems for controlling process fluids. In yet other embodiments, the present technology is directed to systems for transporting process fluids. In other embodiments, the present technology is directed to apparatuses for controlling flow of process fluids.
  • the present systems and manifold assemblies may be used in a wide range of processes such as semiconductor chip fabrication, solar panel fabrication, etc.
  • the invention is a system for processing articles.
  • the system has a first fluid supply configured to supply a first process fluid and a second fluid supply configured to supply a second process fluid.
  • the system has a first apparatus for controlling flow, the first apparatus having an inlet, an outlet, and a bleed port, the inlet of the first apparatus fluidly coupled to the first fluid supply.
  • the system has a second apparatus for controlling flow, the second apparatus having an inlet, an outlet, and a bleed port, the inlet of the second apparatus fluidly coupled to the second fluid supply.
  • the apparatus has first and second mounting substrates, the first mounting substrate having a first vacuum port and a first outlet port, the first apparatus for controlling flow attached to the first mounting substrate such that the bleed port of the first apparatus for controlling flow is fluidly coupled to the first vacuum port and the outlet of the first apparatus for controlling flow is fluidly coupled to the first outlet port.
  • the second mounting substrate has a second vacuum port and a second outlet port, the second apparatus for controlling flow attached to the second mounting substrate such that the bleed port of the second apparatus for controlling flow is fluidly coupled to the second vacuum port and the outlet of the second apparatus for controlling flow is fluidly coupled to the second outlet port.
  • the system has a vacuum manifold fluidly coupled to the first and second vacuum ports, an outlet manifold fluidly coupled to the first and second outlet ports, a vacuum source fluidly coupled to the vacuum manifold, and a processing chamber fluidly coupled to the outlet manifold.
  • the invention is a system for controlling process fluids.
  • the system has a first apparatus for controlling flow, the first apparatus having an inlet, an outlet, and a bleed port, the inlet of the first apparatus configured to receive a first process fluid.
  • the system has a second apparatus for controlling flow, the second apparatus having an inlet, an outlet, and a bleed port, the inlet of the second apparatus configured to receive a second process fluid.
  • the apparatus has first and second mounting substrates, the first mounting substrate having a first vacuum port and a first outlet port, the first apparatus for controlling flow attached to the first mounting substrate such that the bleed port of the first apparatus for controlling flow is fluidly coupled to the first vacuum port and the outlet of the first apparatus for controlling flow is fluidly coupled to the first outlet port.
  • the second mounting substrate has a second vacuum port and a second outlet port, the second apparatus for controlling flow attached to the second mounting substrate such that the bleed port of the second apparatus for controlling flow is fluidly coupled to the second vacuum port and the outlet of the second apparatus for controlling flow is fluidly coupled to the second outlet port.
  • the system has a vacuum manifold fluidly coupled to the first and second vacuum ports and an outlet manifold fluidly coupled to the first and second outlet ports.
  • the invention is a system for transporting process fluids.
  • the system has a plurality of mounting substrates, each mounting substrate having a vacuum port and an outlet port.
  • the system has a vacuum manifold fluidly coupled to the vacuum ports of the plurality of mounting substrates.
  • the system also has an outlet manifold fluidly coupled to the outlet ports of the plurality of mounting substrates.
  • the vacuum manifold has a plurality of primary channels extending along a first longitudinal axis and a plurality of feed channels, the vacuum ports of the plurality of mounting substrates fluidly coupled to the plurality of primary channels via the plurality of feed channels.
  • the outlet manifold has a plurality of primary channels extending along a second longitudinal axis, the first and second longitudinal axes being parallel.
  • the invention is an apparatus for controlling flow of a process fluid.
  • the apparatus has an inlet, an outlet, a bleed port, a flow path extending from the inlet to the outlet, a first valve, a flow restrictor, a second valve, and a mounting portion.
  • the first valve is operably coupled to the flow path and located between the inlet and the outlet, the first valve configured to control flow of a process fluid in the flow path.
  • the flow restrictor has a flow impedance and is operably coupled to the flow path and located between the inlet and the outlet.
  • the second valve is operably coupled to the flow path and located between the inlet and the outlet, the second valve configured to control flow of the process fluid from the flow path to the bleed port.
  • the mounting portion comprises the outlet and the bleed port.
  • the invention is a method of manufacturing articles.
  • the method involves providing a first apparatus for controlling flow of a first process fluid, the first apparatus for controlling flow having a mounting portion.
  • the method further involves providing a first mounting substrate having a surface, the surface having an outlet port and a vacuum port, the outlet port fluidly coupled to an outlet manifold and the vacuum port fluidly coupled to a vacuum manifold.
  • the mounting portion of the first apparatus for controlling flow is secured to the surface of the first mounting substrate.
  • the outlet manifold is fluidly coupled to a processing chamber, and the vacuum manifold is fluidly coupled to a vacuum source.
  • the first process fluid is supplied to the first apparatus for controlling flow.
  • the first process fluid is flowed through the first apparatus for controlling flow.
  • the first process fluid is delivered from the first apparatus for controlling flow to the vacuum port of the first mounting substrate.
  • the first process fluid is discharged through the vacuum manifold to the vacuum source.
  • the first process fluid is delivered from the first apparatus for controlling flow to the outlet port on the first mounting substrate. Finally, a process is performed on an article within the processing chamber.
  • FIG. 1 is a schematic of a system for manufacturing semiconductor devices utilizing one or more apparatuses for controlling flow.
  • FIG. 2 is a schematic of a mass flow controller, the mass flow controller being one of the apparatuses for controlling flow as may be utilized in the process of FIG. 1.
  • FIG. 3 is a perspective view of a plurality of apparatuses for controlling flow and a manifold system as may be utilized in the system of FIG. 1.
  • FIG. 4 is a perspective view of a mass flow controller and a portion of the manifold system, the mass flow controller being one of the apparatuses for controlling flow as may be utilized in the system of FIG. 1.
  • FIG. 5 is a lower perspective view of the mass flow controller and the portion of the manifold system of FIG. 4.
  • FIG. 6 is a left side view of the mass flow controller and the portion of the manifold system of FIG. 4.
  • FIG. 7 is a right side view of the mass flow controller and the portion of the manifold system of FIG. 4.
  • FIG. 8 is a front view of the mass flow controller and the portion of the manifold system of FIG. 4.
  • FIG. 9 is a rear view of the mass flow controller and the portion of the manifold system of FIG. 4.
  • FIG. 10 is a top view of the mass flow controller and the portion of the manifold system of FIG. 4.
  • FIG. 11 is a bottom view of the mass flow controller and the portion of the manifold system of FIG. 4.
  • FIG. 12 is a cross-sectional view of the mass flow controller and the portion of the manifold system of FIG. 8, taken along line XII-XII.
  • FIG. 13 is a perspective view of the manifold system of FIG. 3.
  • FIG. 14 is a top view of the manifold system of FIG. 3.
  • FIG. 15 is a perspective view of a mounting substrate of the manifold system of Fig. 3 and portions of the vacuum and outlet manifolds.
  • FIG. 16 is a bottom perspective view of the mounting substrate of FIG. 15.
  • FIG. 17 is a cross-sectional view of the mounting substrate of FIG. 15, taken along line XVII-XVII.
  • FIG. 18 is a cross-sectional view of the mounting substrate of FIG. 15, taken along line XVIII-XVIII.
  • FIG. 19 is a perspective view of a cradle of the mounting substrate of FIG. 15.
  • FIG. 20 is a top view of a cradle of the mounting substrate of FIG. 15.
  • FIG. 21 is a bottom perspective view of a cradle of the mounting substrate of FIG. 15.
  • FIG. 22 is a perspective view of a first portion of a port block of the mounting substrate of FIG. 15.
  • FIG. 23 is a bottom perspective view of the first portion of the port block of the mounting substrate of FIG. 15.
  • FIG. 24 is a perspective view of a second portion of the port block of the mounting substrate of FIG. 15.
  • FIG. 25 is a bottom perspective view of the second portion of the port block of the mounting substrate of FIG. 15.
  • the present invention is directed to systems for processing articles, these systems having apparatuses for controlling fluid flow.
  • the apparatus may function as a mass flow controller to deliver a known mass flow of gas or liquid to a semiconductor or similar process.
  • Semiconductor fabrication is one industry which demands high performance in control of fluid flows. As semiconductor fabrication techniques have advanced, customers have recognized the need for flow control devices with increased accuracy and repeatability in the mass of the delivered fluid flows. In addition, flow control devices have increased in complexity, utilizing more sophisticated arrangements that require delivery and removal of a variety of process fluids.
  • the present systems enable rapid assembly and maintenance of systems for processing articles by utilizing standardized manifold configurations.
  • Fig. 1 shows a schematic of an exemplary processing system 1000 for processing articles.
  • the processing system 1000 may utilize a plurality of apparatus for controlling flow 100 fluidly coupled to a processing chamber 1300.
  • the plurality of apparatus for controlling flow 100 are used to supply one or more different process fluids to the processing chamber 1300 via an outlet manifold 400.
  • Articles such as semiconductors may be processed within the processing chamber 1300.
  • a valve 1100 isolates the apparatuses for controlling flow 100 from the processing chamber 1300, enabling the apparatuses for controlling flow 100 to be selectively connected or isolated from the processing chamber 1300.
  • the processing chamber 1300 may contain one or more applicators to apply process fluids delivered by the plurality of apparatus for controlling flow 100, enabling selective or diffuse distribution of the fluid supplied by the plurality of apparatus for controlling flow 100.
  • the processing system 1000 may further comprise a vacuum source 1200 which is isolated from the processing chamber 1300 by a valve 1100 to enable evacuation of process fluids or facilitate purging one or more of the apparatus for controlling flow 100 to enable switching between process fluids in the same apparatus for controlling flow 100.
  • Each of the apparatuses for controlling flow 100 may have a separate bleed port which is coupled to a vacuum manifold 500, the vacuum manifold connected to the vacuum source 1200 via a valve 1100.
  • the apparatuses for controlling flow 100 may be mass flow controllers, flow splitters, or any other device which controls the flow of a process fluid in a processing system.
  • valves 1100 may be integrated into the apparatus for controlling flow 100 if so desired. In some implementations this may eliminate the need for certain other valves 1100 in the processing system 1000.
  • Processes that may be performed in the processing system 1000 may include wet cleaning, photolithography, ion implantation, dry etching, atomic layer etching, wet etching, plasma ashing, rapid thermal annealing, furnace annealing, thermal oxidation, chemical vapor deposition, atomic layer deposition, physical vapor deposition, molecular beam epitaxy, laser lift-off, electrochemical deposition, chemical-mechanical polishing, wafer testing, or any other process utilizing controlled volumes of a process fluid.
  • Fig. 2 shows a schematic of an exemplary mass flow controller 101, which is one type of apparatus for controlling flow 100 that may be utilized in the processing system 1000.
  • the mass flow controller 101 has a fluid supply 102 of a process fluid fluidly coupled to an inlet 104.
  • the inlet 104 is fluidly coupled to a proportional valve 120 which is capable of varying the mass and volume of process fluid flowing through the proportional valve 120.
  • the proportional valve 120 meters the mass flow of process fluid which passes to a PI volume 106.
  • the proportional valve 120 is capable of providing proportional control of the process fluid such that it need not be fully open or closed, but instead may have intermediate states to permit control of the mass flow rate of process fluid.
  • the PI volume 106 is fluidly coupled to the proportional valve 120, the PI volume 106 being the sum of all the volume within the mass flow controller 101 between the proportional valve 120 and a flow restrictor 160.
  • a pressure transducer 130 is fluidly coupled to the PI volume 106 to enable measurement of the pressure within the PI volume 106.
  • a shutoff valve 150 is located between the flow restrictor 160 and the proportional valve 120 and may be used to completely halt flow of the process fluid out of the PI volume 106.
  • the flow restrictor 160 may be located between the shutoff valve 150 and the proportional valve 120 in an alternate configuration.
  • the flow restrictor 160 is fluidly coupled to an outlet 110 of the mass flow controller 101.
  • the outlet 110 is fluidly coupled to a valve 1100 or directly to the processing chamber 1300.
  • the flow restrictor 160 is located between the shutoff valve 150 and the outlet 110.
  • the shutoff valve 150 is located between the flow restrictor 160 and the outlet 110.
  • a bleed valve 180 is coupled to the PI volume 106 and to a bleed port 190.
  • the bleed valve 180 may be a proportional valve, on/off valve, or any other type of valve suitable for controlling fluid flow.
  • a second flow restrictor may be incorporated between the PI volume and the bleed port 190.
  • first shutoff valve 150 Internal to the first shutoff valve 150 is a valve seat and a closure member. When the apparatus 100 is delivering process fluid, the first shutoff valve 150 is in an open state, such that the valve seat and the closure member are not in contact. This permits flow of the process fluid and provides a negligible restriction to fluid flow. When the first shutoff valve 150 is in a closed state the closure member and the valve seat are biased into contact by a spring, stopping the flow of process fluid through the first shutoff valve 150.
  • the flow restrictor 160 is used, in combination with the proportional valve 120, to meter flow of the process fluid.
  • the flow restrictor 160 provides a known restriction to fluid flow.
  • the first characterized flow restrictor 160 may be selected to have a specific flow impedance so as to deliver a desired range of mass flow rates of a given process fluid.
  • the flow restrictor 160 has a greater resistance to flow than the passages upstream and downstream of the flow restrictor 160.
  • the mass flow controller 101 comprises one or more P2 pressure transducers downstream of the flow restrictor 160 and the shutoff valve 150.
  • the P2 pressure transducer is used to measure the pressure differential across the flow restrictor 160.
  • the P2 pressure downstream of the flow restrictor 160 may be obtained from another apparatus 100 connected to the processing chamber, with the readings communicated to the mass flow controller 101.
  • temperature sensors may be employed to further enhance the accuracy of the mass flow controller 101. They may be mounted in the base of the mass flow controller 101 near the PI volume 106. Additional temperature sensors may be employed in a variety of locations, including adjacent the proportional valve 120, the pressure transducer 130, the shutoff valve 150, and the bleed valve 180.
  • FIG. 3 a perspective view of a plurality of apparatuses for controlling flow
  • each of the apparatuses 100 are mass flow controllers 101, but each of the apparatuses 100 could be different devices.
  • mass flow controller 101 need be identical. Some may support different fluids, different ranges of flow capability, or any other variation necessary to implement the desired process.
  • the mass flow controllers 101 are mounted to the manifold system 300.
  • Figs. 4-12 show a single mass flow controller 101 in greater detail, along with a portion 301 of the manifold system 300.
  • the portion 301 provides the necessary attachment features to mount the mass flow controller 101 or other apparatuses 100 in a standardized configuration.
  • the manifold system enables both vacuum and outlet manifolds to be connected with a minimum of complexity as will be described in greater detail below.
  • the mass flow controller 101 comprises a base 103 formed of a first portion 105 and a second portion 107.
  • the base 103 is unitary and monolithic, while in other instances the base 103 may be formed of more than two portions.
  • the base 103 comprises an inlet 104 and an outlet 110, a flow path extending from the inlet 104 to the outlet 110.
  • the inlet 104 is fluidly coupled to a fluid supply 102 as discussed above.
  • Process fluids flow from the inlet 104 to the outlet 110 along the flow path, the inlet 104 being referred to as upstream and the outlet 110 being referred to as downstream, as this is the ordinary direction for fluid flow during operation of the mass flow controller 101.
  • Both the inlet 104 and the outlet 110 lie in a plane M-M which extends through the center of the mass flow controller
  • the base 103 further comprises valve caps 113 which close off passages.
  • the valve caps 113 are used to facilitate manufacturing of the base 103 and aid in assembly of the mass flow controller 101.
  • the inlet 104 is fluidly coupled to an inlet control valve 151, the inlet control valve 151 serving to control the flow of fluid into the mass flow controller 101.
  • the primary function of the inlet control valve 151 is to provide guaranteed shutoff of the mass flow controller 101 for maintenance, service, calibration, etc.
  • the inlet control valve 151 may be manually or automatically operated. In some embodiments, the inlet control valve 151 may be omitted.
  • an integrated particle filter 108 Downstream of the inlet control valve 151, an integrated particle filter 108 is installed in the first portion 105 of the base 103.
  • the integrated particle filter 108 may be omitted. Alternatively, it may be located upstream of the inlet control valve 151 or elsewhere in the flow path. In yet other embodiments, the integrated particle filter 108 may be omitted.
  • the P0 volume 109 comprises all volume in the flow path between the inlet control valve 151 and a valve seat 122 of the proportional control valve.
  • the proportional valve 120 comprises the valve seat 122 and a closure member 121.
  • the proportional valve is configured to transition from a closed state to an open state as well as any intermediate position between the open and the closed states. This allows a variable volume of gas or liquid to pass the proportional valve 120.
  • Downstream of the proportional valve 120 is a shutoff valve 150 and a characterized restrictor 160.
  • the shutoff valve 150 may be upstream or downstream of the characterized restrictor 160.
  • the volume between the proportional valve 120 and the characterized restrictor 160 is referred to as a PI volume 106.
  • the PI volume 106 comprises all volume in the flow path between the valve seat 122 of the proportional valve 120 and the characterized restrictor 160.
  • a bleed valve 180 and a PI pressure transducer 130 are fluidly coupled to the PI volume 106 between the proportional valve 120 and the characterized restrictor 160.
  • the bleed valve 180 comprises a closure member 181 and a valve seat 182.
  • the PI pressure transducer 130 measures the pressure of the fluid in the PI volume 106.
  • the bleed valve 180 is configured to vent fluid from the PI volume 106 to a bleed port 190.
  • the bleed port 190 must be connected to a vacuum manifold to dispose of process fluids. The vacuum manifold is discussed below in greater detail.
  • the characterized restrictor 160 is located downstream of the shutoff valve 150 and upstream of the outlet 110 as discussed above.
  • the characterized restrictor 160 is configured such that it provides a restriction to fluid flow to provide a pressure differential between the PI volume 106 and a P2 volume 111.
  • the P2 volume 111 comprises the volume of the flow path between the characterized restrictor 160 and the outlet 110.
  • the P2 volume 111 is fluidly coupled to a P2 pressure transducer 132, the P2 pressure transducer 132 measuring the pressure of the fluid in the P2 volume 111.
  • the restriction to fluid flow of the characterized restrictor 160 may also be referred to as a flow impedance, the flow impedance being sufficiently high that the pressure drop across the characterized restrictor 160 can be measured using the PI and P2 pressure transducers 130, 132.
  • the characterized restrictor 160 may be upstream of the shutoff valve 150. In some embodiments, the characterized restrictor 160 may be at least partially located within the shutoff valve 150. In yet other embodiments, the shutoff valve 150 may be omitted.
  • the PI and P2 pressure transducers 130, 132 may also be omitted in certain embodiments.
  • one or more of the P0, PI, and P2 pressure transducers 131, 130, 132 may be differential pressure sensors, and may be fluidly coupled to more than one of the P0, PI, and P2 volumes 109, 106, 111 to permit differential pressure measurement between the P0, PI, and P2 volumes 109, 106, 111.
  • the bleed valve 180 controls flow through a bleed passage 181 that connects the bleed valve 180 to the bleed port 190.
  • This bleed passage 181 may take any required path to reach a mounting portion 112.
  • the mounting portion 112 forms a portion of the base 103 and has a surface 114 comprising the bleed port 190 and the outlet 110. In a preferred embodiment, the surface 114 of the mounting portion 112 is planar. The mounting portion 112 enables connection of the mass flow controller 101 to the portion 301 of the manifold system 300.
  • the portion 301 of the manifold system 300 comprises a portion 501 of the vacuum manifold 500 and a portion 401 of the outlet manifold 400.
  • the portion 301 of the manifold system 300 further comprises a mounting substrate 310.
  • the 3 310 provides the mechanical connection for the mounting portion 112 of the mass flow controller 101.
  • the mounting substrate 310 provides both structural strength and rigidity to the mass flow controller 101 and ensures robust fluid connection between the two components.
  • the mounting portion 112 of the mass flow controller 101 is configured to engage the mounting substrate 310 to fluidly couple the outlet 110 and the bleed port 190 to the vacuum manifold 500 and the outlet manifold 400.
  • the surface 114 of the mounting portion 112 may incorporate features necessary to ensure that the bleed port 190 and outlet 110 can be adequately sealed to ensure liquid and/or gas tight connections between the mounting portion 112 and the mounting substrate 310. These features may include recesses or any other feature necessary to provide room for sealing features, seals, or other components that provide a fluid-tight connection.
  • the manifold system 300 comprises a plurality of portions 301, each portion 301 being substantially identical.
  • Each of the portions 301 comprises a portion 401 of the outlet manifold 400 and a portion 501 of the vacuum manifold 500.
  • the portions 401 of the outlet manifold 400 collectively form the outlet manifold 400 and the portions 501 of the vacuum manifold 500 collectively form the vacuum manifold 500.
  • Each portion 301 comprises a mounting substrate 310.
  • the vacuum manifold 500 extends along a longitudinal axis A-A, the longitudinal axis A- A being coaxial with a plurality of primary channels 502.
  • the longitudinal axis A-A extends perpendicular to the plane M-M, which extends through the inlet 104 and the outlet 110 of the mass flow controller 101.
  • a first one of the portions 301 of the manifold system 300 may not comprise a primary channel 502 so that it may be sealed and may terminate the vacuum manifold 500.
  • the first one of the portions 301 may also comprise a primary channel 502 that is coupled to another tubing system or may be coupled to the vacuum source 1200 as discussed above.
  • a last one of the portions 301 comprises a primary channel 502 that is fluidly coupled to the vacuum source 1200 to ensure that the vacuum manifold 500 is under vacuum.
  • the primary channels 502 are coupled to a plurality of feed channels 504 via a plurality of tee fittings 506.
  • the feed channels 504 extend along a longitudinal axis C-C, the longitudinal axis C-C being perpendicular to the longitudinal axis A-A.
  • the longitudinal axis C-C extends parallel to the plane M-M, which extends through the inlet 104 and the outlet 110 of the mass flow controller 101.
  • the feed channels 504 couple to the mounting substrates 310 and permit fluid connection of the mounting substrates 310 to the plurality of primary channels 502.
  • the primary channels 502 and the feed channels 504 may be pipe nipples, lengths of pipe, or other tubular members that conduct fluids. They may be coupled to the mounting substrates 310 and the tee fittings 506 via any known method, including threading, welding, soldering, slip fits, compression fits, mounting flanges, monolithic construction, and the like. Although the primary channels 502 are shown in two parts, each primary channel 502 may be integrally formed such that it extends between adjacent tee fittings 506.
  • the feed channels 504 may not extend perpendicular to the longitudinal axis A-A and may be angled with respect to the longitudinal axis A-A at an angle other than 90 degrees.
  • the outlet manifold 400 extends along a longitudinal axis B-B, the longitudinal axis B-B being parallel to the longitudinal axis A-A and spaced from the longitudinal axis A-A.
  • the longitudinal axis B-B extends perpendicular to the plane M-M, which extends through the inlet 104 and the outlet 110 of the mass flow controller 101.
  • the outlet manifold 400 comprises a plurality of primary channels 402 which connect the mounting substrates 310.
  • each primary channel 402 may be integrally formed such that it extends between adjacent mounting substrates 310.
  • the longitudinal axis B-B may not extend parallel to the longitudinal axis A-A and may be angled with respect to the longitudinal axis A-A.
  • FIG. 15-18 the portions 301 of the manifold system 300 are discussed in greater detail.
  • a single portion 301 is shown in Figs. 15-18, but the other portions 301 are substantially identical.
  • the single portion 301 comprises the portion 401 of the outlet manifold 400 and the portion 5101 of the vacuum manifold.
  • the portion 301 also comprises the mounting substrate 310.
  • the mounting substrate 310 comprises a cradle 320 and a port block 330.
  • the port block 330 comprises a first portion 340 and a second portion 350.
  • the first portion 340 comprises an outlet port 341 while the second portion 350 comprises a vacuum port 351.
  • the port block 330 is formed as a single unitary monolithic component, with the first and second portions 340, 350 being portions of a single component. In other embodiments, such as the one shown, the port block 330 is formed such that the first and second portions 340, 350 are individual components.
  • the mounting substrate 310 further comprises a 312, the surface 312 being substantially planar.
  • the cradle 320 and the port block 330 each form a portion of the surface 312, permitting the mounting portion 112 of the mass flow controller 101 to seal against the surface 312.
  • the outlet port 341 and the vacuum port 351 are formed into the surface 312.
  • Four mounting holes 322 are provided in the cradle 320 to permit attachment of an apparatus for controlling flow 100 such as the mass flow controller 101.
  • Two bolts 314 are provided for attaching the mounting substrate 310 to another object such as a bench, frame, or other structure within the factory where the system is installed. These bolts 314 may be installed in counterbored through-holes which extend through the cradle 320.
  • FIG. 17 a cross-section along the line XVII- XVII of Fig. 15 is shown.
  • the portion 301 is shown cut through the outlet manifold 400 and associated portions of the mounting substrate 310.
  • the outlet manifold 400 extends along the axis B-B.
  • the cradle 320 supports the outlet manifold 400 and the port block 320, with the first portion 340 of the port block 330 being visible.
  • the fluid flow path from the outlet port 341 of the first portion 340 of the port block 330 to the primary channels 402 of the outlet manifold 400 is best shown in this view.
  • Fig. 18 shows a cross-section along the line XVIII- XVIII of Fig. 15.
  • the portion 301 is shown sectioned through the first and second portions 340, 350 of the port block 330.
  • the vacuum port 351 of the second portion 350 is fluidly coupled to one of the feed channels 504 of the vacuum manifold 500. Fluid from the vacuum port 351 travels into the second portion 350, turning a right angle and then proceeding along the feed channel 504 until it reaches the tee fitting 506.
  • the outlet port 341 of the first portion 340 is also shown, with the fluid turning at a right angle until it reaches the outlet manifold 400.
  • the cradle 320 supports the port block 330 such that the surface 312 is substantially planar, ensuring effective sealing of the mass flow controller 101 with the mounting substrate 110.
  • the cradle 320 has mounting holes 322 as discussed previously, which are used to attach apparatuses for controlling flow 100.
  • Counterbored holes 324 are used to attach the cradle 320 to a substrate such as a frame, table, or other component to provide mechanical support for the mounting substrate 310 and the apparatus 100.
  • the cradle 320 also has a first side 325, a second side 326, a third side 327, and a fourth side 328. The first side 325 and the second side 326 are opposite one another and the third side 327 and fourth side 328 are opposite one another.
  • a first slot 332 extends through the cradle 320 from the first side 325 toward the second side 326.
  • a second slot 333 extends through the cradle 320 from the second side 326 toward the first side 325.
  • the first and second slots 332, 333 extend from the first side 325 to the second side 326.
  • a third slot 334 extends through the cradle 320 from the third side 327 toward the fourth side 328.
  • a fourth slot 335 extends through the cradle 320 from the fourth side 328 toward the third side 327.
  • Collectively, the third and fourth slots 334, 335 extend from the third side 327 to the fourth side 328.
  • the first and second sides 325, 326 are perpendicular to the third and fourth sides 327, 328.
  • the first and second slots 332, 333 receive the primary channels 402 while the third slot 334 receives the feed channel 504.
  • the fourth slot 335 is left unoccupied.
  • the outlet manifold 400 extends through the first and second slots 332, 333 and the vacuum manifold 500 extends through one of the third and fourth slots 334, 335.
  • Providing the fourth slot 335 allows greater flexibility in manifold configuration. It is conceived that the vacuum manifold 500 might extend through the fourth slot 335 instead of the third slot 334. It is also conceivable that a third port could be added to the port block 330 to enable connection of three manifolds, allowing different process chambers to be served by the same equipment or providing multiple vacuum manifolds for different fluids or different purposes.
  • the first and second slots 332, 333 are wider than the third and fourth slots 334, 335.
  • the first and second slots 332, 333 are perpendicular to the third and fourth slots 334, 335.
  • the slots 332, 333, 334, 335 could be of the same width or the first and second slots 332, 333 could be narrower than the third and fourth slots 334, 335.
  • the slots 332, 333, 334, 335 also need not be parallel or perpendicular to one another and may be arranged at different angles to accommodate manifold channels which are angled at other than right angles.
  • Figs. 22 and 23 show the second portion 350 of the port block 330 with the portion 501 of the vacuum manifold 500.
  • the vacuum port 351 of the second portion is located on a top surface 352, which can be clearly seen in Fig. 22.
  • the feed channel 504, tee fitting 506, and the primary channels 502 can be seen extending from the second portion 350.
  • the second portion 350 is configured to fit within the third slot 334 and has a width which is approximately equal to the width of the third slot 334 as measured from a first side 353 to a second side 354.
  • the second portion 350 has a height which is substantially equal to a depth of the third slot 334.
  • Figs. 24 and 25 show the first portion 340 of the port block 330 with the portion 401 of the outlet manifold 400.
  • the vacuum port 341 is located on a top surface 342, which can be best seen in Fig. 24.
  • the primary channels 402 can be seen extending from first and second ends 343, 344.
  • the first portion 340 has a width which is approximately equal to the width of the first and second slots 332, 334, the width being measured from a third side 345 to a fourth side 346.
  • the first portion 340 has a height which is substantially equal to a depth of the first and second slots 332, 333.
  • an apparatus for controlling flow 100 is provided, the apparatus 100 comprising a mounting portion 112.
  • a mounting substrate 312 is also provided, the mounting substrate having a surface 312 having an outlet port 341 and a vacuum port 351 formed therein.
  • the outlet port 341 is fluidly coupled to an outlet manifold 400 and the vacuum port 351 is fluidly coupled to a vacuum manifold 500.
  • the outlet manifold 400 is fluidly coupled to a processing chamber 1300 and the vacuum manifold 500 is fluidly coupled to a vacuum source 1200.
  • a process fluid is supplied to the apparatus 100, the process fluid flows through the apparatus 100 and is delivered to a bleed port 190.
  • the process fluid then flows from the bleed port 190 to the vacuum port 351 because the mounting portion 112 of the apparatus 100 is mounted to the mounting substrate 312 such that the vacuum port 351 is in fluid communication with the bleed port 190.
  • the outlet port 341 is in fluid communication with the outlet 110 of the apparatus 100.
  • Process fluid flows from the vacuum port 351 to the vacuum manifold 500 and on to the vacuum source 1200.
  • the process fluid flows through the apparatus 100 and is delivered to the outlet 110.
  • the process fluid flows from the outlet 110 through the outlet port 341 of the mounting substrate and on to the outlet manifold 400.
  • Process fluid then flows to the processing chamber 1300.
  • the process fluid is used to perform a process on an article within the processing chamber.
  • the article being processed is a semiconductor device or is manufactured into a semiconductor device as a result of the processing performed in the method.
  • the process fluid is flowed through the vacuum port 351 before it is flowed through the outlet port 341. In other embodiments the process fluid flows through both the vacuum port 351 simultaneously with flowing through the outlet port 341. In yet other embodiments, the process fluid flows through the outlet port 341 before it flows through the vacuum port 351. In yet further embodiments, a plurality of apparatuses 100 and mounting substrates 312 may be utilized. In these embodiments, a plurality of process fluids may be used, or the same process fluid may be used in more than one apparatus 100. In those embodiments utilizing a plurality of apparatuses 100, more than one apparatus 100 may be active simultaneously. In some embodiments, more than one process fluid may flow through the corresponding vacuum ports 351 and outlet ports 341 simultaneously.

Abstract

Des systèmes de traitement d'articles sont essentiels pour la fabrication de semi-conducteurs. Selon un mode de réalisation, l'invention concerne un système comprenant une pluralité d'alimentations en fluide conçues pour fournir des fluides de traitement, une pluralité d'appareils destinés à réguler le débit, une pluralité de substrats de support, un collecteur pneumatique en communication fluidique avec la pluralité de substrats de support, un collecteur de sortie en communication fluidique avec la pluralité de substrats de support, une source de vide en communication fluidique avec le collecteur pneumatique et une chambre de traitement en communication fluidique avec le collecteur de sortie. La pluralité d'appareils de régulation de débit comportent une prise de prélèvement et une sortie. Les sorties de la pluralité d'appareils sont en communication fluidique avec des orifices de sortie correspondants de la pluralité de substrats de support. Les prises de prélèvement de la pluralité d'appareils sont en communication fluidique avec les orifices d'aspiration correspondants de la pluralité de substrats de support.
PCT/US2022/016286 2021-03-03 2022-02-14 Système de régulation de débit de fluide comprenant un ensemble collecteur WO2022186971A1 (fr)

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KR1020237031210A KR20230150309A (ko) 2021-03-03 2022-02-14 매니폴드 조립체를 포함하는 유체 유동 제어 시스템
JP2023553151A JP2024512898A (ja) 2021-03-03 2022-02-14 マニホールドアセンブリを備える流体流れ制御システム

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US63/155,861 2021-03-03

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5653259A (en) * 1994-10-17 1997-08-05 Applied Biosystems, Inc. Valve block
US6298881B1 (en) * 1999-03-16 2001-10-09 Shigemoto & Annett Ii, Inc. Modular fluid handling assembly and modular fluid handling units with double containment
US20080302434A1 (en) * 2007-06-11 2008-12-11 Lam Research Corporation Flexible manifold for integrated gas system gas panels
US7784496B2 (en) * 2007-06-11 2010-08-31 Lam Research Corporation Triple valve inlet assembly
US20190243393A1 (en) * 2016-06-30 2019-08-08 Reno Technologies, Inc. Flow control system, method, and apparatus

Family Cites Families (282)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2666297A (en) 1950-03-14 1954-01-19 Elmer C Skousgaard Container and discharge valve therefor
US3335748A (en) 1964-09-15 1967-08-15 Henry B Peter Adjustable control for metered flow
US3271994A (en) 1965-04-19 1966-09-13 Jered Ind Inc Fluid flow comparator for use in calibrating fluid flow orifices
US3504692A (en) 1966-05-31 1970-04-07 Massachusetts Inst Technology Pneumatic oscillator
US3491946A (en) 1966-06-28 1970-01-27 Ibm Fluid-actuated synchronizing apparatus
US3453861A (en) 1967-04-25 1969-07-08 Us Navy Square wave fluid pressure generator
US3559482A (en) 1968-11-27 1971-02-02 Teledyne Inc Fluid flow measuring apparatus
US3570807A (en) 1969-01-14 1971-03-16 Bell Aerospace Corp Electromechanical control valve
US3841520A (en) 1969-04-04 1974-10-15 Airco Inc Flame arresting vent valve
US3807456A (en) 1970-06-25 1974-04-30 Trw Inc Hydraulic controller including rotary valve
JPS5110899Y2 (fr) 1971-02-03 1976-03-24
US3814541A (en) 1971-11-24 1974-06-04 Delta Controls Ltd Fluid supply apparatus
JPS4974000U (fr) 1972-10-16 1974-06-26
US3910113A (en) 1972-11-20 1975-10-07 William R Brown Method of selectively varying the differential output and overall performance characteristics of a proportional differential pressure producing fluid flow device
JPS5090559U (fr) 1973-12-19 1975-07-31
JPS5340417Y2 (fr) 1973-12-20 1978-09-29
US4026657A (en) 1974-09-05 1977-05-31 Textron, Inc. Sintered spherical articles
US4015626A (en) 1976-01-22 1977-04-05 Thordarson, Inc. Constant flow valve for low flow rates
US4096746A (en) 1977-02-25 1978-06-27 The Perkin-Elmer Corporation Flow controller-flow sensor assembly for gas chromatographs and the like
US4275752A (en) 1978-09-22 1981-06-30 Collier Nigel A Fluid flow apparatus and method
US4304263A (en) 1979-02-09 1981-12-08 Choate J Robert Fluid control system
US4203465A (en) 1979-03-27 1980-05-20 General Motors Corporation Precision pressure control valve
US4253156A (en) 1979-06-22 1981-02-24 The United States Of America As Represented By The Administrator Of The National Aeronautics And Space Administration Automatic flowmeter calibration system
DE2929389C2 (de) 1979-07-20 1984-05-17 Machinefabriek Mokveld B.V., 2800 Gouda Regelventil
US4315523A (en) 1980-03-06 1982-02-16 American Flow Systems, Inc. Electronically controlled flow meter and flow control system
EP0061856B1 (fr) 1981-04-01 1987-08-26 LUCAS INDUSTRIES public limited company Mesure du débit massique d'air entrant dans une machine à combustion interne
US4462915A (en) 1981-09-23 1984-07-31 Oil Process Systems, Inc. Method and system for filtering cooking oil
US4527600A (en) 1982-05-05 1985-07-09 Rockwell International Corporation Compressed natural gas dispensing system
FR2543321B1 (fr) 1983-03-22 1985-08-16 Electricite De France Dispositif de commande d'un debit de fluide, notamment de fluide radioactif
US4576043A (en) 1984-05-17 1986-03-18 Chevron Research Company Methods for metering two-phase flow
US4669052A (en) 1985-07-02 1987-05-26 Motorola, Inc. Apparatus and method for calibrating a sensor
DE3538828A1 (de) 1985-10-31 1987-05-07 Druva Gmbh Armaturengrundkoerper, insbesondere als teil eines druckminderers
US4718443A (en) 1987-02-06 1988-01-12 Conoco Inc. Mass flowmeter apparatus
US5100551A (en) 1987-03-27 1992-03-31 Pall Corporation Segmented filter disc with slotted support and drainage plate
GB8711931D0 (en) 1987-05-20 1987-06-24 British Petroleum Co Plc Filtration/coalescence
CA1309954C (fr) 1987-07-29 1992-11-10 Yasuo Yamada Desaerateur pour materiaux particulaires
GB8720356D0 (en) 1987-08-28 1987-10-07 Thorn Emi Flow Measurement Ltd Fluid meter
US4918995A (en) 1988-01-04 1990-04-24 Gas Research Institute Electronic gas meter
US4858643A (en) 1988-03-14 1989-08-22 Unit Instruments, Inc. Fluid flow stabilizing apparatus
US4796651A (en) 1988-03-30 1989-01-10 LeRoy D. Ginn Variable gas volume flow measuring and control methods and apparatus
NL9000339A (nl) 1990-02-13 1991-09-02 System Engineering & Component Drukvalreductie-inrichting, en klep voorzien van een drukvalreductie-inrichting.
US5419133A (en) 1989-09-05 1995-05-30 Schneider; Edward T. High speed thermochemical actuator
US5080131A (en) 1989-09-26 1992-01-14 Lintec Co., Ltd. Mass flow controller
DE3936619A1 (de) 1989-11-03 1991-05-08 Man Nutzfahrzeuge Ag Verfahren zum einspritzen eines brennstoffes in einen brennraum einer luftverdichtenden, selbstzuendenden brennkraftmaschine, sowie vorrichtungen zur durchfuehrung dieses verfahrens
US5044199A (en) 1989-11-13 1991-09-03 Dxl International, Inc. Flowmeter
JPH03156509A (ja) 1989-11-14 1991-07-04 Stec Kk マスフローコントローラ
US5123439A (en) 1990-02-01 1992-06-23 Industrial Ceramics Engineering Valve body ceramic liners
US5237523A (en) 1990-07-25 1993-08-17 Honeywell Inc. Flowmeter fluid composition and temperature correction
US5100100A (en) 1990-09-12 1992-03-31 Mks Instruments, Inc. Fluid control and shut off valve
US5052363A (en) 1990-10-22 1991-10-01 Ford Motor Company EGR control valve having ceramic elements
JPH079036Y2 (ja) 1990-11-13 1995-03-06 東京エレクトロン東北株式会社 縦型熱処理炉
US5138869A (en) 1990-12-14 1992-08-18 Novapure Corporation In-line detector system for real-time determination of impurity concentration in a flowing gas stream
US5583282A (en) 1990-12-14 1996-12-10 Millipore Investment Holdings Limited Differential gas sensing in-line monitoring system
US5259243A (en) 1991-01-04 1993-11-09 Dxl International, Inc. Flow sensor
US5062446A (en) 1991-01-07 1991-11-05 Sematech, Inc. Intelligent mass flow controller
US5359878A (en) 1991-02-26 1994-11-01 Dxl International, Inc. Apparatus and method for in-line calibration verification of mass flow meters
JPH07111367B2 (ja) 1991-02-26 1995-11-29 ディーエクスエル・インターナショナル・インコーポレーテッド 流量センサおよびその検査方法
US5114447A (en) 1991-03-12 1992-05-19 Mott Metallurgical Corporation Ultra-high efficiency porous metal filter
US5152483A (en) 1991-05-13 1992-10-06 Seop Maeng Golf bag with support stand
WO1992021006A2 (fr) 1991-05-17 1992-11-26 Unit Instruments, Inc. Procede et appareil de traduction du signal d'un debitmetre massique
US5321992A (en) 1991-09-26 1994-06-21 Dxl Usa Measurement of gas flows with enhanced accuracy
US5311762A (en) 1991-12-16 1994-05-17 Dxl Usa Flow sensor calibration
DE69212129T2 (de) 1991-12-18 1997-01-23 Pierre Delajoud Massenströmungsmesser mit einschnürendem Element
US5187972A (en) 1992-01-17 1993-02-23 Clean Air Engineering, Inc. Gas monitor
US5305638A (en) 1992-03-20 1994-04-26 Dxl International, Inc. Mass flowmeter having non-adjustable flow splitter
US5190068A (en) 1992-07-02 1993-03-02 Brian Philbin Control apparatus and method for controlling fluid flows and pressures
US5297427A (en) 1992-09-03 1994-03-29 Alicat Scientific, Inc. Wide-range laminar flowmeter
US5439026A (en) 1992-12-11 1995-08-08 Tokyo Electron Limited Processing apparatus and flow control arrangement therefor
US5329966A (en) 1993-03-08 1994-07-19 Vici Metronics Incorporated Gas flow controller
DE69405533T2 (de) 1994-03-10 1998-01-22 Gi Corp Gasleitungssystem für einen CVD-Reaktor
US5511585A (en) 1994-03-31 1996-04-30 The Lee Company Method and device for providing fluid resistance within a flow passageway
US5624409A (en) 1994-06-10 1997-04-29 Fluidsense Corporation Variable-pulse dynamic fluid flow controller
US5730181A (en) 1994-07-15 1998-03-24 Unit Instruments, Inc. Mass flow controller with vertical purifier
US5549272A (en) 1994-08-11 1996-08-27 Johnson Service Company Combination pressure pulsation damper and check valve depressor
US5542284A (en) 1994-10-18 1996-08-06 Queen's University At Kingston Method and instrument for measuring differential oxygen concentration between two flowing gas streams
FI100409B (fi) 1994-11-28 1997-11-28 Asm Int Menetelmä ja laitteisto ohutkalvojen valmistamiseksi
US5660207A (en) 1994-12-29 1997-08-26 Tylan General, Inc. Flow controller, parts of flow controller, and related method
JP3291161B2 (ja) 1995-06-12 2002-06-10 株式会社フジキン 圧力式流量制御装置
US5725024A (en) 1995-09-11 1998-03-10 Pgi International, Ltd. Manifold valve having controlled vent port integral with flange
US6026847A (en) 1995-10-11 2000-02-22 Reinicke; Robert H. Magnetostrictively actuated valve
US5711786A (en) 1995-10-23 1998-01-27 The Perkin-Elmer Corporation Gas chromatographic system with controlled sample transfer
US5762086A (en) 1995-12-19 1998-06-09 Veriflo Corporation Apparatus for delivering process gas for making semiconductors and method of using same
KR100232112B1 (ko) 1996-01-05 1999-12-01 아마노 시게루 가스공급유닛
US5804717A (en) 1996-04-05 1998-09-08 Mks Instruments, Inc. Mass flow transducer having extended flow rate measurement range
US5868159A (en) 1996-07-12 1999-02-09 Mks Instruments, Inc. Pressure-based mass flow controller
JP3580645B2 (ja) 1996-08-12 2004-10-27 忠弘 大見 圧力式流量制御装置
US5944048A (en) 1996-10-04 1999-08-31 Emerson Electric Co. Method and apparatus for detecting and controlling mass flow
US5911238A (en) 1996-10-04 1999-06-15 Emerson Electric Co. Thermal mass flowmeter and mass flow controller, flowmetering system and method
US6293310B1 (en) 1996-10-30 2001-09-25 Unit Instruments, Inc. Gas panel
US5918616A (en) 1996-11-15 1999-07-06 Sanfilippo; James J. Apparatus and method of controlling gas flow
US6062256A (en) 1997-02-11 2000-05-16 Engineering Measurements Company Micro mass flow control apparatus and method
US6062246A (en) 1997-04-08 2000-05-16 Hitachi Metals Ltd. Mass flow controller and operating method thereof
US5865205A (en) 1997-04-17 1999-02-02 Applied Materials, Inc. Dynamic gas flow controller
JP3737869B2 (ja) 1997-05-13 2006-01-25 シーケーディ株式会社 プロセスガス供給ユニット
US5904170A (en) 1997-05-14 1999-05-18 Applied Materials, Inc. Pressure flow and concentration control of oxygen/ozone gas mixtures
US6074691A (en) 1997-06-24 2000-06-13 Balzers Aktiengesellschaft Method for monitoring the flow of a gas into a vacuum reactor
US5917066A (en) 1997-07-16 1999-06-29 Mott Metallurgical Corporation Inline ultra-high efficiency filter
US5935418A (en) 1997-08-29 1999-08-10 Exxon Research And Engineering Co. Slurry hydroprocessing
JPH11119835A (ja) 1997-10-13 1999-04-30 Horiba Ltd マスフローコントローラおよび集積化流量制御装置
US6026834A (en) 1997-10-17 2000-02-22 Azima; Faramarz Fluid mass flow controller device and method
US5970801A (en) 1997-12-30 1999-10-26 Bear Medical Systems, Inc. Variable orifice flow sensor
JP3932389B2 (ja) 1998-01-19 2007-06-20 Smc株式会社 マスフローコントローラの自己診断方法
JPH11212653A (ja) 1998-01-21 1999-08-06 Fujikin Inc 流体供給装置
JP3557087B2 (ja) 1998-02-06 2004-08-25 シーケーディ株式会社 マスフローコントローラ流量検定システム
US6080219A (en) 1998-05-08 2000-06-27 Mott Metallurgical Corporation Composite porous media
JP2000018407A (ja) 1998-07-02 2000-01-18 Ckd Corp プロセスガス供給ユニット
US5988211A (en) 1998-07-06 1999-11-23 Randolph W. Cornell I.V. flow controller
US6116269A (en) 1998-07-07 2000-09-12 Fasco Controls Corporation Solenoid pressure transducer
US6152162A (en) 1998-10-08 2000-11-28 Mott Metallurgical Corporation Fluid flow controlling
US6269692B1 (en) 1999-02-01 2001-08-07 Dxl Usa Inc. Mass flow measuring assembly having low pressure drop and fast response time
WO2000063756A1 (fr) 1999-04-16 2000-10-26 Fujikin Incorporated Dispositif d'alimentation en fluide du type derivation parallele, et procede et dispositif de commande du debit d'un systeme de pression du type a fluide variable utilise dans ledit dispositif
US6210482B1 (en) 1999-04-22 2001-04-03 Fujikin Incorporated Apparatus for feeding gases for use in semiconductor manufacturing
US6119710A (en) 1999-05-26 2000-09-19 Cyber Instrument Technologies Llc Method for wide range gas flow system with real time flow measurement and correction
US6425281B1 (en) 1999-07-12 2002-07-30 Unit Instruments, Inc. Pressure insensitive gas control system
US6138708A (en) 1999-07-28 2000-10-31 Controls Corporation Of America Mass flow controller having automatic pressure compensator
US6352001B1 (en) 1999-08-30 2002-03-05 General Electric Company Non-iterative method for obtaining mass flow rate
US6799603B1 (en) 1999-09-20 2004-10-05 Moore Epitaxial, Inc. Gas flow controller system
US6314991B1 (en) 2000-03-02 2001-11-13 Rajinder S. Gill Mass flow controller
US6303501B1 (en) 2000-04-17 2001-10-16 Applied Materials, Inc. Gas mixing apparatus and method
WO2002008844A1 (fr) 2000-07-08 2002-01-31 Fugasity Corporation Soupape de regulation de debit pour une masse fluide et procede de mise en oeuvre
FI20001694A0 (fi) 2000-07-20 2000-07-20 Asm Microchemistry Oy Menetelmä ohutkalvon kasvattamiseksi substraatille
AU2001277984A1 (en) 2000-07-25 2002-02-05 Fugasity Corporation Small internal volume fluid mass flow control apparatus
AU2001286619A1 (en) 2000-08-22 2002-03-04 Fugasity Corporation Fluid mass flow meter with substantial measurement range
US6642281B1 (en) 2000-09-01 2003-11-04 Exxonmobil Research And Engineering Company Fischer-tropsch process
US6539968B1 (en) 2000-09-20 2003-04-01 Fugasity Corporation Fluid flow controller and method of operation
US6832628B2 (en) 2000-10-11 2004-12-21 Flowmatrix, Inc. Variable pressure regulated flow controllers
US6439254B1 (en) 2000-11-30 2002-08-27 Industrial Technology Research Institute Mass flow controller automation method and related system
US6631334B2 (en) 2000-12-26 2003-10-07 Mks Instruments, Inc. Pressure-based mass flow controller system
US6564824B2 (en) 2001-04-13 2003-05-20 Flowmatrix, Inc. Mass flow meter systems and methods
US6752166B2 (en) 2001-05-24 2004-06-22 Celerity Group, Inc. Method and apparatus for providing a determined ratio of process fluids
US6655408B2 (en) 2001-06-13 2003-12-02 Applied Materials, Inc. Tunable ramp rate circuit for a mass flow controller
JP5069839B2 (ja) 2001-10-12 2012-11-07 ホリバ エステック,インコーポレーテッド 質量流量装置を作製および使用するためのシステム及び方法
JP2003280745A (ja) 2002-03-25 2003-10-02 Stec Inc マスフローコントローラ
US7809473B2 (en) 2002-06-24 2010-10-05 Mks Instruments, Inc. Apparatus and method for pressure fluctuation insensitive mass flow control
GB2419677A (en) 2002-06-24 2006-05-03 Mks Instr Inc Pressure fluctuation insensitive mass flow controller
US6948508B2 (en) 2002-06-24 2005-09-27 Mks Instruments, Inc. Apparatus and method for self-calibration of mass flow controller
US7136767B2 (en) 2002-06-24 2006-11-14 Mks Instruments, Inc. Apparatus and method for calibration of mass flow controller
US6868862B2 (en) 2002-06-24 2005-03-22 Mks Instruments, Inc. Apparatus and method for mass flow controller with a plurality of closed loop control code sets
US6712084B2 (en) 2002-06-24 2004-03-30 Mks Instruments, Inc. Apparatus and method for pressure fluctuation insensitive mass flow control
US7552015B2 (en) 2002-06-24 2009-06-23 Mks Instruments, Inc. Apparatus and method for displaying mass flow controller pressure
JP3973605B2 (ja) 2002-07-10 2007-09-12 東京エレクトロン株式会社 成膜装置及びこれに使用する原料供給装置、成膜方法
CN1688948B (zh) 2002-07-19 2010-05-26 布鲁克斯器具有限公司 在质量流动控制器中用于压力补偿的方法和装置
US7431045B2 (en) 2002-08-28 2008-10-07 Horiba Stec, Co., Ltd. Flow restrictor
JP4594728B2 (ja) 2002-08-28 2010-12-08 ホリバ ステック, インコーポレイテッド より高い正確度の圧力に基づく流れコントローラ
JP4283884B2 (ja) 2002-10-21 2009-06-24 シーケーディ株式会社 ガス集積弁
JP2004157719A (ja) 2002-11-06 2004-06-03 Stec Inc マスフローコントローラ
EP1601900A2 (fr) 2003-03-07 2005-12-07 Swagelok Company Soupape a butee reglable
WO2004085309A1 (fr) 2003-03-24 2004-10-07 Japan Science And Technology Agency Procede synthetique haute efficacite destine a une nanostructure en carbone, appareil et nanostructure en carbone
WO2004085703A1 (fr) 2003-03-25 2004-10-07 Tokyo Electron Limited Appareil et procede de traitement
JP2004302914A (ja) 2003-03-31 2004-10-28 Advanced Energy Japan Kk 一次側圧力のセンサを具えたマスフローコントローラ
JP4224492B2 (ja) 2003-06-09 2009-02-12 シーケーディ株式会社 圧力制御システム及び流量制御システム
ATE468421T1 (de) 2003-06-27 2010-06-15 Sundew Technologies Llc Vorrichtung und verfahren zur steuerung des dampfdrucks einer chemikalienquelle
KR100418684B1 (ko) 2003-06-27 2004-02-14 주식회사 현대교정인증기술원 반도체 공정가스용 차압식 유량 제어기
JP4204400B2 (ja) 2003-07-03 2009-01-07 忠弘 大見 差圧式流量計及び差圧式流量制御装置
JP4351495B2 (ja) 2003-07-16 2009-10-28 株式会社堀場エステック 流量比率制御装置
US8376312B2 (en) 2003-08-28 2013-02-19 Horiba, Ltd. Flow restrictor
JP2005079141A (ja) 2003-08-28 2005-03-24 Asm Japan Kk プラズマcvd装置
JP4235076B2 (ja) 2003-10-08 2009-03-04 東京エレクトロン株式会社 半導体製造装置および半導体製造方法
KR101176825B1 (ko) 2003-10-09 2012-08-24 브룩스 인스트러먼트, 엘엘씨, 밸브 조립체
JP4186831B2 (ja) 2004-02-03 2008-11-26 日立金属株式会社 質量流量制御装置
US7370674B2 (en) 2004-02-20 2008-05-13 Michael Doyle Modular fluid distribution system
EP2365412B1 (fr) 2004-02-27 2012-10-03 Horiba Stec, Co., Ltd. Limiteur de débit
US7628860B2 (en) 2004-04-12 2009-12-08 Mks Instruments, Inc. Pulsed mass flow delivery system and method
US7628861B2 (en) 2004-12-17 2009-12-08 Mks Instruments, Inc. Pulsed mass flow delivery system and method
US20060060139A1 (en) 2004-04-12 2006-03-23 Mks Instruments, Inc. Precursor gas delivery with carrier gas mixing
US20050252449A1 (en) 2004-05-12 2005-11-17 Nguyen Son T Control of gas flow and delivery to suppress the formation of particles in an MOCVD/ALD system
CN100408900C (zh) 2004-05-20 2008-08-06 喜开理株式会社 气体供给集成单元和气体单元的增设方法
CN1704615A (zh) 2004-06-01 2005-12-07 斯瓦戈洛克公司 流体致动器
JP4086057B2 (ja) 2004-06-21 2008-05-14 日立金属株式会社 質量流量制御装置及びこの検定方法
JP2006009969A (ja) 2004-06-25 2006-01-12 Kitz Sct:Kk 集積化ガス制御装置用流路ブロックとその製造方法並びに集積化ガス制御装置
US7216019B2 (en) 2004-07-08 2007-05-08 Celerity, Inc. Method and system for a mass flow controller with reduced pressure sensitivity
KR100653710B1 (ko) 2004-12-14 2006-12-04 삼성전자주식회사 질량 유량 제어기
US20060130755A1 (en) 2004-12-17 2006-06-22 Clark William R Pulsed mass flow measurement system and method
US7370664B2 (en) 2005-01-31 2008-05-13 Swagelok Company Flow control device
CN101305230A (zh) 2005-02-22 2008-11-12 斯瓦戈洛克公司 阀与促动器组件
US7474968B2 (en) 2005-03-25 2009-01-06 Mks Instruments, Inc. Critical flow based mass flow verifier
US7757554B2 (en) 2005-03-25 2010-07-20 Mks Instruments, Inc. High accuracy mass flow verifier with multiple inlets
US7726630B2 (en) 2005-05-20 2010-06-01 Parker-Hannifin Corporation Solenoid valve
TWI552797B (zh) 2005-06-22 2016-10-11 恩特葛瑞斯股份有限公司 整合式氣體混合用之裝置及方法
JP2009501878A (ja) 2005-07-13 2009-01-22 スウエイジロク・カンパニー 作動の方法および設備
JP2007034667A (ja) 2005-07-27 2007-02-08 Surpass Kogyo Kk 流量コントローラ、これに用いるレギュレータユニット、バルブユニット
JP2007041870A (ja) 2005-08-03 2007-02-15 Horiba Stec Co Ltd ガス流量制御方法
TWI329136B (en) 2005-11-04 2010-08-21 Applied Materials Inc Apparatus and process for plasma-enhanced atomic layer deposition
KR100725098B1 (ko) 2005-11-17 2007-06-04 삼성전자주식회사 반도체 제조설비의 유량조절기 오동작 감지장치 및 그 방법
US7680399B2 (en) 2006-02-07 2010-03-16 Brooks Instrument, Llc System and method for producing and delivering vapor
JP4788920B2 (ja) 2006-03-20 2011-10-05 日立金属株式会社 質量流量制御装置、その検定方法及び半導体製造装置
US20070227659A1 (en) 2006-03-31 2007-10-04 Tokyo Electron Limited Plasma etching apparatus
CN101438091B (zh) 2006-06-02 2012-05-23 喜开理株式会社 气体供给单元和气体供给系统
CN101583916B (zh) 2006-10-03 2011-11-09 株式会社堀场Stec 质量流量控制器
US8744784B2 (en) 2006-11-02 2014-06-03 Horiba Stec, Co., Ltd. Diagnostic mechanism in differential pressure type mass flow controller
WO2008069227A1 (fr) 2006-12-05 2008-06-12 Horiba Stec, Co., Ltd. Contrôleur d'écoulement, procédé de test de dispositif de mesure d'écoulement, système de test de contrôleur d'écoulement et appareil de fabrication de semiconducteurs
JP4642115B2 (ja) 2006-12-12 2011-03-02 株式会社堀場エステック 流量比率制御装置
US7706925B2 (en) 2007-01-10 2010-04-27 Mks Instruments, Inc. Integrated pressure and flow ratio control system
US7846497B2 (en) 2007-02-26 2010-12-07 Applied Materials, Inc. Method and apparatus for controlling gas flow to a processing chamber
US20080305014A1 (en) 2007-06-07 2008-12-11 Hitachi Kokusai Electric Inc. Substrate processing apparatus
JP5079401B2 (ja) 2007-06-25 2012-11-21 サーパス工業株式会社 圧力センサ、差圧式流量計及び流量コントローラ
JP5001757B2 (ja) 2007-08-31 2012-08-15 シーケーディ株式会社 流体混合システム及び流体混合装置
LV13661B (en) 2007-09-12 2008-02-20 Aleksejs Safronovs Method and device to compress gaseos fuel for vehicles filling
JP2009079667A (ja) 2007-09-26 2009-04-16 Tokyo Electron Ltd ガス供給装置及び半導体製造装置
JP4974000B2 (ja) 2007-10-01 2012-07-11 日立金属株式会社 質量流量制御装置及び実ガスの質量流量制御方法
US7874208B2 (en) 2007-10-10 2011-01-25 Brooks Instrument, Llc System for and method of providing a wide-range flow controller
US7693606B2 (en) 2007-12-21 2010-04-06 Rosemount Inc. Diagnostics for mass flow control
JP4585035B2 (ja) 2007-12-27 2010-11-24 株式会社堀場エステック 流量比率制御装置
JP5181956B2 (ja) 2008-03-03 2013-04-10 株式会社リコー 電子写真装置
US8504318B2 (en) 2008-03-05 2013-08-06 Brooks Instruments, Llc System, method and computer program for determining fluid flow rate using a pressure sensor and a thermal mass flow sensor
US8205629B2 (en) 2008-04-25 2012-06-26 Applied Materials, Inc. Real time lead-line characterization for MFC flow verification
JP2009300403A (ja) 2008-06-17 2009-12-24 Horiba Stec Co Ltd 質量流量計及びマスフローコントローラ
US8340827B2 (en) 2008-06-20 2012-12-25 Lam Research Corporation Methods for controlling time scale of gas delivery into a processing chamber
US8291857B2 (en) 2008-07-03 2012-10-23 Applied Materials, Inc. Apparatuses and methods for atomic layer deposition
TWI378490B (en) 2008-07-04 2012-12-01 Delta Electronics Inc Fluorescent lamp with adjustable color temperature
JP5408916B2 (ja) 2008-07-08 2014-02-05 サーパス工業株式会社 差圧式流量計及び流量コントローラ
US8187381B2 (en) 2008-08-22 2012-05-29 Applied Materials, Inc. Process gas delivery for semiconductor process chamber
US7905139B2 (en) 2008-08-25 2011-03-15 Brooks Instrument, Llc Mass flow controller with improved dynamic
US7826986B2 (en) 2008-09-26 2010-11-02 Advanced Energy Industries, Inc. Method and system for operating a mass flow controller
JP5091821B2 (ja) 2008-09-29 2012-12-05 株式会社堀場エステック マスフローコントローラ
JP4705140B2 (ja) 2008-10-06 2011-06-22 株式会社堀場エステック 質量流量計及びマスフローコントローラ
JP2010109303A (ja) 2008-10-31 2010-05-13 Horiba Ltd 材料ガス濃度制御装置
JP4700095B2 (ja) 2008-11-03 2011-06-15 シーケーディ株式会社 ガス供給装置、ブロック状フランジ
NL2003389A (en) 2008-11-04 2010-05-06 Asml Holding Nv Reverse flow gas gauge proximity sensor.
US7891228B2 (en) 2008-11-18 2011-02-22 Mks Instruments, Inc. Dual-mode mass flow verification and mass flow delivery system and method
JP2010169657A (ja) 2008-12-25 2010-08-05 Horiba Stec Co Ltd 質量流量計及びマスフローコントローラ
JP5346628B2 (ja) 2009-03-11 2013-11-20 株式会社堀場エステック マスフローコントローラの検定システム、検定方法、検定用プログラム
JP5337542B2 (ja) 2009-03-12 2013-11-06 株式会社堀場エステック マスフローメータ、マスフローコントローラ、それらを含むマスフローメータシステムおよびマスフローコントローラシステム
US8793082B2 (en) 2009-07-24 2014-07-29 Mks Instruments, Inc. Upstream volume mass flow verification systems and methods
JP5101581B2 (ja) 2009-08-25 2012-12-19 株式会社堀場エステック 流量制御装置
WO2011040409A1 (fr) 2009-10-01 2011-04-07 株式会社堀場エステック Mécanisme de mesure de débit et régulateur de débit massique
KR101737147B1 (ko) 2009-10-01 2017-05-17 가부시키가이샤 호리바 에스텍 유량 측정 기구, 매스 플로우 콘트롤러 및 압력 센서
TWI435196B (zh) 2009-10-15 2014-04-21 Pivotal Systems Corp 氣體流量控制方法及裝置
US8265795B2 (en) 2009-11-05 2012-09-11 Horiba Stec, Co., Ltd. Mass flow controller
CN102096420B (zh) 2009-12-15 2015-01-14 株式会社堀场Stec 质量流量控制器
US9223318B2 (en) 2009-12-25 2015-12-29 Horiba Stec, Co., Ltd. Mass flow controller system
JP5189603B2 (ja) 2010-01-13 2013-04-24 Ckd株式会社 流量コントローラ及び比例電磁弁
JP2011171337A (ja) 2010-02-16 2011-09-01 Hitachi Kokusai Electric Inc 基板処理装置
US8343258B2 (en) 2010-03-30 2013-01-01 Agilent Technologies, Inc. Apparatus and method for controlling constant mass flow to gas chromatography column
JP5607501B2 (ja) 2010-11-08 2014-10-15 株式会社堀場エステック マスフローコントローラ
US9400004B2 (en) 2010-11-29 2016-07-26 Pivotal Systems Corporation Transient measurements of mass flow controllers
US8460753B2 (en) 2010-12-09 2013-06-11 Air Products And Chemicals, Inc. Methods for depositing silicon dioxide or silicon oxide films using aminovinylsilanes
KR101599343B1 (ko) 2011-05-10 2016-03-03 가부시키가이샤 후지킨 유량 모니터 부착 압력식 유량 제어 장치
GB201108854D0 (en) 2011-05-26 2011-07-06 Spp Process Technology Systems Uk Ltd Mass flow controller monitoring
JP5090559B2 (ja) 2011-06-08 2012-12-05 株式会社堀場エステック マスフローコントローラ
JP5933936B2 (ja) 2011-06-17 2016-06-15 株式会社堀場エステック 流量測定システム、流量制御システム、及び、流量測定装置
US8770215B1 (en) 2011-07-20 2014-07-08 Daniel T. Mudd Low flow injector to deliver a low flow of gas to a remote location
US8915262B2 (en) 2011-08-09 2014-12-23 Hitachi Metals, Ltd. Mass flow controller algorithm with adaptive valve start position
US9448564B2 (en) 2013-02-15 2016-09-20 Reno Technologies, Inc. Gas delivery system for outputting fast square waves of process gas during semiconductor processing
US9958302B2 (en) 2011-08-20 2018-05-01 Reno Technologies, Inc. Flow control system, method, and apparatus
US9188989B1 (en) 2011-08-20 2015-11-17 Daniel T. Mudd Flow node to deliver process gas using a remote pressure measurement device
US20160041564A1 (en) 2012-08-20 2016-02-11 Daniel T. Mudd Reverse flow mode for regulating pressure of an accumulated volume with fast upstream bleed down
US20160018828A1 (en) 2014-04-29 2016-01-21 Daniel T. Mudd Pressure-based mass flow controller with reverse flow mode for fast bleed down
JP5809012B2 (ja) 2011-10-14 2015-11-10 株式会社堀場エステック 流量制御装置、流量測定機構、又は、当該流量測定機構を備えた流量制御装置に用いられる診断装置及び診断用プログラム
JP2013088944A (ja) 2011-10-14 2013-05-13 Horiba Stec Co Ltd 流量制御装置、流量測定機構、又は、当該流量測定機構を備えた流量制御装置に用いられる診断装置及び診断用プログラム
JP5873681B2 (ja) 2011-10-14 2016-03-01 株式会社堀場エステック 流量制御装置、流量制御装置に用いられる診断装置及び診断用プログラム
US20130118609A1 (en) 2011-11-12 2013-05-16 Thomas Neil Horsky Gas flow device
US9027585B2 (en) 2011-12-13 2015-05-12 Hitachi Metals, Ltd. Adaptive pressure insensitive mass flow controller and method for multi-gas applications
US9471066B2 (en) 2012-01-20 2016-10-18 Mks Instruments, Inc. System for and method of providing pressure insensitive self verifying mass flow controller
JP5715969B2 (ja) 2012-01-24 2015-05-13 株式会社堀場エステック 流体抵抗デバイス
JP5868219B2 (ja) 2012-02-29 2016-02-24 株式会社フジキン 流体制御装置
WO2013134147A1 (fr) 2012-03-07 2013-09-12 Illinois Tool Works Inc. Système et procédé pour fournir un régulateur de débit massique à auto-validation et un débitmètre
WO2013134136A1 (fr) 2012-03-07 2013-09-12 Illinois Tool Works Inc. Système et procédé pour améliorer la précision d'une mesure de la vitesse de décroissance dans un organe de commande de débit massique
WO2013134140A1 (fr) 2012-03-07 2013-09-12 Illinois Tool Works Inc. Système et procédé pour réduire les perturbations d'écoulement et améliorer la précision d'une mesure de la vitesse de décroissance dans un organe de commande de débit massique
KR101938928B1 (ko) 2012-03-07 2019-01-15 일리노이즈 툴 워크스 인코포레이티드 질량 유량 제어기 또는 질량 유량 측정기의 실시간 측정과 제로 옵셋 및 제로 드리프트의 보정을 위한 감쇠율 측정을 사용하는 시스템과 방법
JP5887188B2 (ja) 2012-04-12 2016-03-16 株式会社堀場エステック 流体制御用機器
US8985152B2 (en) 2012-06-15 2015-03-24 Novellus Systems, Inc. Point of use valve manifold for semiconductor fabrication equipment
JP5947659B2 (ja) 2012-08-06 2016-07-06 株式会社堀場エステック 流量制御装置
WO2014040002A2 (fr) 2012-09-10 2014-03-13 Mudd Daniel T Régulateur de débit massif à pression
US10031005B2 (en) 2012-09-25 2018-07-24 Mks Instruments, Inc. Method and apparatus for self verification of pressure-based mass flow controllers
US9090972B2 (en) * 2012-12-31 2015-07-28 Lam Research Corporation Gas supply systems for substrate processing chambers and methods therefor
JP6081800B2 (ja) 2013-01-07 2017-02-15 株式会社堀場エステック 流体制御弁及びマスフローコントローラ
WO2014152755A2 (fr) 2013-03-14 2014-09-25 Christopher Max Horwitz Dispositif de commande d'écoulement de gaz basé sur la pression et présentant un auto-étalonnage dynamique
US9446331B2 (en) 2013-03-15 2016-09-20 Taiwan Semiconductor Manufacturing Co., Ltd. System and method for dispensing photoresist
US9940004B2 (en) 2013-03-15 2018-04-10 Gregory Mayworm Methods and systems for predicting and evaluating coffee characteristics
US9891124B2 (en) 2013-05-24 2018-02-13 Hitachi Metals, Ltd. Pressure sensor, and mass flow meter, and mass flow controller using same
US9574712B2 (en) 2013-08-15 2017-02-21 Trillium Transportation Fuels, Llc System and method of automatically ending the filling of a gas transport module or other gas transport
US9335768B2 (en) 2013-09-12 2016-05-10 Lam Research Corporation Cluster mass flow devices and multi-line mass flow devices incorporating the same
KR102210858B1 (ko) 2013-10-21 2021-02-02 가부시키가이샤 호리바 에스텍 유체 제어 밸브
EP3218626B1 (fr) 2014-11-15 2023-11-15 Versum Materials US, LLC Bloc de distribution perfectionné à zone morte minimale
US9920844B2 (en) 2014-11-26 2018-03-20 Lam Research Corporation Valve manifold deadleg elimination via reentrant flow path
US10957561B2 (en) 2015-07-30 2021-03-23 Lam Research Corporation Gas delivery system
US20170082076A1 (en) 2015-09-17 2017-03-23 Caterpillar Inc. Pressure regulator for fuel supply system
US10838437B2 (en) 2018-02-22 2020-11-17 Ichor Systems, Inc. Apparatus for splitting flow of process gas and method of operating same
US10679880B2 (en) 2016-09-27 2020-06-09 Ichor Systems, Inc. Method of achieving improved transient response in apparatus for controlling flow and system for accomplishing same
JP7061808B2 (ja) 2017-03-15 2022-05-02 株式会社フジキン 継手および流体制御装置
CN113994460A (zh) 2019-04-15 2022-01-28 朗姆研究公司 用于气体输送的模块部件系统

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5653259A (en) * 1994-10-17 1997-08-05 Applied Biosystems, Inc. Valve block
US6298881B1 (en) * 1999-03-16 2001-10-09 Shigemoto & Annett Ii, Inc. Modular fluid handling assembly and modular fluid handling units with double containment
US20080302434A1 (en) * 2007-06-11 2008-12-11 Lam Research Corporation Flexible manifold for integrated gas system gas panels
US7784496B2 (en) * 2007-06-11 2010-08-31 Lam Research Corporation Triple valve inlet assembly
US20190243393A1 (en) * 2016-06-30 2019-08-08 Reno Technologies, Inc. Flow control system, method, and apparatus

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